US2302450A - Filter - Google Patents
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- US2302450A US2302450A US343062A US34306240A US2302450A US 2302450 A US2302450 A US 2302450A US 343062 A US343062 A US 343062A US 34306240 A US34306240 A US 34306240A US 2302450 A US2302450 A US 2302450A
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- Prior art keywords
- sand
- gravel
- layer
- backwash
- box
- Prior art date
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D24/00—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
- B01D24/002—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof with multiple filtering elements in parallel connection
- B01D24/005—Filters being divided into a plurality of cells or compartments
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D24/00—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
- B01D24/007—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof with multiple filtering elements in series connection
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D24/00—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
- B01D24/02—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof with the filter bed stationary during the filtration
- B01D24/20—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof with the filter bed stationary during the filtration the filtering material being provided in an open container
- B01D24/22—Downward filtration, the filter material being supported by pervious surfaces
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D24/00—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
- B01D24/46—Regenerating the filtering material in the filter
- B01D24/4631—Counter-current flushing, e.g. by air
- B01D24/4636—Counter-current flushing, e.g. by air with backwash shoes; with nozzles
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D24/00—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
- B01D24/46—Regenerating the filtering material in the filter
- B01D24/4631—Counter-current flushing, e.g. by air
- B01D24/4642—Counter-current flushing, e.g. by air with valves, e.g. rotating valves
- B01D24/4647—Counter-current flushing, e.g. by air with valves, e.g. rotating valves with a rectilinear movement of the closing means
Definitions
- This invention relates to lter apparatus, and
- the object of this invention is to overcome these disadvantages and to provide a filter bed with layers which will at all times remain in proper relationship.
- the invention consists in disposing between the gravel layer and sand layer, a porous layer of such characteristics that the gravel and sand layers remain as such Without intermingling with each other, though the sand particles or the gravel particles intermingle with each other separately, without intermixing.
- a porous layer of such characteristics that the gravel and sand layers remain as such Without intermingling with each other, though the sand particles or the gravel particles intermingle with each other separately, without intermixing.
- Such an intermediate layer must have the attribute that each constituent part has a specic gravity such as to resist the forces and actions of the backwash cleaning fluid and while allowing the fluid to pass, itself remaining in position, whereby the gravel remains coniined rbelow and the sand remains confined above, without intermixing with the constituents of the intermediate layer.
- Such a stabilizing intermediate layer is to fulfill the purpose of the graduated gravel bed, namely to distribute the ascending water, while the various layers of differently sized gravels remain in their position.
- These layers are usually arranged with the largest size gravel lowermcst. Due to the gradual decrease in size, the resistance to the uprising water increases as the size of the gravel decreases, giving therefore more uniform distribution of water with each size.
- a quantity of differently sized sands have previously been used in their respective layers. As there is a tendency of the light gravel to rise and float, with the fine sand directly on the gravel of 1/8 to le", a mixing of A the same took place, and in the hope of avoiding this, deep beds were utilized.
- the invention enables shallow gravel beds and relatively shallow sand beds to be used, by reason of thev provision of the intermediate layer of porous material of a constituency of relatively heavy specific gravity.
- the use of such an intermediate layer permits a higher velocity for the use of backwash water.
- Such an intermediate layer may beY of magnetite placed on the nest or top layer of gravel, and next below to the ne. eiective sand.
- the relative high specic gravity of the magnetite prevents the boiling of the gravel into it, and the intermixing of the fine sand with the magnetite.
- the Weight of such over intermediate layer thus acts to keep the strata formation of the layers of gravel and sand.
- the invention comprises a comparatively shallow graduated gravel bed supported by a perforated plate with a total area of openingsin the plate such as will cause Wash Water to pass through the openings at highvelocity, with a layer of heavier specific gravity constituents between the gravel layer and a superposed sand layer, whereby the intermediate layer acts as the nal point of water distribution into the iine sand uppermost layer, permitting the sand to boil andthe dirt to be washed out Without the intermediate layer moving or rising.
- an outlet cleaner or dirty water take-off box, may discharge from each compartment the impurities thus separated, as a direct rflow ⁇ from below upwardly.
- Fig. 1 is a perspective View partly in section of part of a lter apparatus, with a plurality of vertical compartments.
- Fig. 2 a detail View of the backwash valve movable to close the lower end opening of each vertical compartment.
- Fig. 3 is a vertical section through one vertical compartment showing the superposed layers of iilter material upon the perforated plate, in relation to the end opening,
- Fig. 4 is a horizontal sectional detail of a pluralit;r of compartments, showing the dirty water take-oil box in one position in respect thereto.
- Fig. is a similar View with the dirty water take-off box in another position
- Fig. 6 is a similar View with the dirty water take-olf box in still another position.
- the lter apparatus there shown, is formed of a bottom wall IU, side walls I I and I2, end walls not being shown.
- vertical partitions I3 Transversely of the apparatus, and perpendicular to the side walls I I and I2, are vertical partitions I3 which extend from side wall to side wall and divide the apparatus whatever may be its width between sidewall and sidewall, and whatever may be its length between endwall and endwall, into separate vertical compartments.
- suitable means I4 are provided for supporting perforated plates I5 which are horizontally disposed and form a perforated support extending from sidewall II to sidewall I2.
- Such means Ill may be secured to the vertical partitions and to the perforated plates.
- Angle irons I4A and MB support the plate I5, but any other suitable means may be provided, as the plate may be supported in any other suitable manner, as long as it is arranged about one-third or one-fourth up from the bottom wall I0.
- the vertical partitions are embedded in the bottom wall I0 but any other suitable iixing means may be utilized.
- the endwall II has a plurality of circular openings I6, spaced from each other, so that the center of said circular openings is eccentric with the geometrical center of the conguration formed by the perforated plate I5, the bottom I0 and the twointervening parts ISA and ISB of the partitions I3.
- the center is indicated by I1. Absolute accuracy of the disposition of the centers is not necessary, as the opening I6 can be arranged anywhere within the parts I5, I0 and I3A and I3B.
- a back wash valve guide I9 is arranged forming an eiliuent channel, which latter is adjacent the sidewall Il, and these guide walls I3 guide a valve which is movable longitudinally from end to end of the apparatus.
- the vertical partitions I3, are provided at their upper ends with horizontally disposed plates 25 and upon them the dirty water take-oir' box 3! having two shoes 3
- the dirty water take-off box 3!) is moved from end to end of the apparatus, preferably periodically, to cover the open top of the vertical compartment which is being supplied at its bottom with washing water, and by means not shown in the drawing.
- the irst improvement consists in providing each vertical compartment with an intermediate layer ⁇ of material of relatively high speciiic gravity between the layers of graded gravel and the layer of sand.
- three layers of gravel are shown, indicated by 40, 4I and 42.
- the lowermost layer 4U has gravel of 1/2" to
- the next superposed layer 4I is of gravel
- the valve 2B to 1/4
- the uppermost superposed layer 42 of gravel is of 1A," to 1/3".
- These gravel layers are held down by a layer of magnetite 43 or the like, of about 1/3 to j/16; and nally the top layer 4A is of sand.
- This sand layer extends only partially towards the uppermost ends I3c of the partitions, whereby a space is provided between the top surface of the sand and the horizontal partition 25.
- Magnetite has a higher specic gravity than gravel or sand, and thereby it acts as a stable intermediate layer stabilizing the gravel and sand layers.
- the second improvement consists in the dirty water take-off box 30, in that it is connected with a suction producing apparatus (not shown) by a pipe 56, so that a suction action causes the impurities washed from the sand to be drawn into the dirty water take-off box 30.
- the box 30 has shoes 3
- the vacuum action serves to draw the box down against the plate, and the liquid above the box serves to press the box down upon the plate.
- two walls 33 and 34 incline upwardly and merge into a horizontal wall 35 having spaced openings 3S, which communicate with a conduit 31 which is in communication with the pipe 50.
- suction is applied, the impurities resting upon the top sand layer or the boiling dirty water, are drawn into the space 38 of the box 30, and then into the conduit 31, and pipe 50 to some suitable place of discharge.
- Figure 4 shows the relative position of the box 3E) in respect to one compartment, the suction box being on.
- This suction action and the consequent cleaning is contrary to the normal ltering action which has a descending action in that the fluid to be ltered is above the top sand layer and as the fluid descends through the top sand and layers below the same, the eiiluent finally reaches the space in the compartment below the perforated plate, and discharges through the opening I3 and into the eluent channel, leaving the impurities or other constituents in adsorption with the sand.
- This upward filter-cleaning action is clearly seen in Figures 4 and 5. It will be understood that while the cleansing action takes place, filtering is interrupted for the time being.
- the arrows 53 and 54 in Figures 4 and 5 show the normally downward filtering action taking place.
- the opening I6 is provided with arrows 55 which show that the washing water enters the opening I6, and this fluid then rises through the gravel layers and layer of magnetite and top layer of sand, taking the adhering impurities with it until sucked in by the box 30 .as described. It is seen that there is a joint action between the vacuum action of the box 30 and the upward back wash action, brought about by the registering of the valve opening with the opening I6 of that particular vertical compartment.
- the intermediate layerv prevents interminglingof the gravel with the sand and, by virtue of its higher specic gravity yet porous characteristic, permits the passage of high-velocity fluidv therethrough without itself losing its layer-like or strata 'formation.
- this intermediate layer acts in the nature of a porous wall formed of material having a specific gravity higher than either the gravel below or vthe sand above, in whatever direction the iiow of fluid therethrough may be.
- leaden bullets of suitable size can be used, orany vother material whose specific gravity is such that it is higher than the gravel particles to prevent them from rising to intermingle with the sand, and higher than the sand Aparticles to prevent the material of the intermediate layer from rising into the sand layer and mixing therewith.
- weighted intermediate layer permits only the top sand layer to boil, withl the top surface of the sand normally'below the top edges of the vertical partitions.
- the sand particles thus entrained can vbe easily substituted by new sand particles' ⁇ supplied to take the place of those removed.
- the provision of the said space reduces the removal of the sand to a minimum.
- a filter bed constructedin accordance with the present invention in which a dirty water take-oi box removes the dirty water when the lter-bed is being subjected to backwashing from below upwardly, can be used in sewage treatment plants and will produce uniformly clean final effluents, the sand bed being a perfect floccing apparatus gathering the minute floc in a layer at the surface of the sand; such a bed can also be used in water treatment to remove algae and amorphous matter at high filter rates, and is especially adapted to filtration of water prior to the slow sand iilters because of the capacity and efliciency of the bed for removing solids, thus permitting an increased capacity and less frequent cleaning of the slow sand filters.
- the filter bed is especially adapted to swimming pools and similar purification installations because of the simple low pressure automatic operation and can easily be provided with means for chlorine dispersion. Furthermore the filter can be used for the recovery of products now going to waste, as
- filter apparatus including a plurality of vertical compartments containing a lter bed for each of said compartments, comprising gravel strata in the lower portion of said compartments, a layer of sand in the upper portion of said compartments, and an intermediate layer of a specific gravity higher than the gravel and sand interposed between said gravel strata and said layer of sand for preventing intermingling of said sand' and gravelduring the cleaning operation of said iilter bed, means 'for periodically?
- backwash cleaning said filterinaterial from theunderside of saidv compartments upwardly means-supplying saidfbackwash cleaning means with backwash liquid, means straddling only the top of the compartment being cleaned forreceiving the backwash water, and leavingadjacent compartments uncovered,'and inlet and outlet filtering liquid means.
- filtering apparatus including a iilter bed consisting of superposed layers of gravel and sand; an inlet for the unfiltered liquid supplied to and above the filter bed and an outlet for the filtered liquid coming from below the filter bed, said Iilter bed being between said inlet and outlet, the combination of backwash supply means below the filter bed, backwash outlet means above said lter bed, and between said backwash supply and outlet means therefor, and a layer of material disposed between said sand and gravel and having a specific gravity higher than that of said sand for preventing intermixture of the gravel with the sand both during the filtering and during the backwashing action.
- filtering apparatus including a plurality of vertical compartments, each containing a filter bed comprising superposed layers of gravel and of sand, and an intermediate layer of material of higher specific gravity than said sand interposed between said first named layers for preventing intermingling of said sand and said gravel during the movement of the liquid in an upward direction through said lter bed, means for periodically backwash cleaning said ltering material from the underside of said compartments, suction removal means of the dirty wash-water at the upper end of the.
- a filter apparatus having a bottom, side and end walls including a plurality of open top channels parallel with each other from end Wall to end wall, a horizontal transverse perforated plate in each channel intermediate its top and bottom, a filter bed supported by each plate, said lter bed consisting of superposed layers of material graduated in respect to specic gravity, one of said interposed layers being of higher specific gravity than the layer above it, in combination therewith of a launder at right angles to the channels having an oriiice communicating with each channel into which filtered liquor from below the plate of the channel enters, backwash means travelling in the launder for forcing a required portion of fluid through an orifice and upwardly from the bottom and through the plate of a channel, means over the channel being back- Washed for removal from the top of the channel of the dirty Wash water as produced by the backwash means without intermingling of such dirty wash water with the supernatant and unltered liquid of adjacent channels, means connecting the backwash means with the removal means, means for moving the backwash means and removal means in unison from
- a filter apparatus having a bottom, side and end walls, a plurality of partitions extending vertically upwardly from said bottom and spaced from each other from end wall to end wall and extending from side wall to side wall, horizontally disposed perforated Walls intermediate the top and bottom ends of said partitions, and a filter material held on said perforated Walls, the combination therewith of horizontally aligned top plates upon each upper end of the said partitions, a dirty water take-off box having enclosing walls spaced substantially equal to the space between the aligned top plates for forming a closed space over two adjacent partitions, a pair of shoes on said box spaced the distance between said top plates and extending over said top plates -for sliding on said top plates, said pair of spaced shoes forming a seal with a pair of said spaced top plates when the box covers the open end of adjacent partitions, means supplying the iluid to be ltered above said partitions and said box, and means supplying a fluid below the filter material for passage to
Description
NOV. 1.7, 1942. Y 'W C .LAUGHLlN FlLTER Filed June 29, 1940 vigil-:112201951071212 BY 3. WJ
TTOR EK Patented Nov. 17, 1942 UNITED STATES ?TSENT OFFICE FILTER,
William C. Laughlin, New York, N. Y.
Application June 29, 1940, Serial No. 343,062
7 Claims.
This invention relates to lter apparatus, and
more particularly to the form in which separate vertical transverse compartments are provided with cleaning material and which are periodically subjected to a cleaning. Embodiments of this type are described and shown in my co-pending application, Ser. No. 325,100, iled March 2l, 1940.
The objections to the use of gravel and sand layer filters is that the backWash Water serves to churn the grave] and sand to such an extent that intermingling of gravel and sand results, rendering the lter bed useless or so inefficient as to require replacement.
The object of this invention is to overcome these disadvantages and to provide a filter bed with layers which will at all times remain in proper relationship.
The invention consists in disposing between the gravel layer and sand layer, a porous layer of such characteristics that the gravel and sand layers remain as such Without intermingling with each other, though the sand particles or the gravel particles intermingle with each other separately, without intermixing. Such an intermediate layer must have the attribute that each constituent part has a specic gravity such as to resist the forces and actions of the backwash cleaning fluid and while allowing the fluid to pass, itself remaining in position, whereby the gravel remains coniined rbelow and the sand remains confined above, without intermixing with the constituents of the intermediate layer.
The use of such a stabilizing intermediate layer is to fulfill the purpose of the graduated gravel bed, namely to distribute the ascending water, while the various layers of differently sized gravels remain in their position. These layers are usually arranged with the largest size gravel lowermcst. Due to the gradual decrease in size, the resistance to the uprising water increases as the size of the gravel decreases, giving therefore more uniform distribution of water with each size. Also usually there is a layer of line sand above the gravel layer. The finer the sand particles, the greater the boiling of the same on the up current of the cleaning water. Instead of one layer of sand, a quantity of differently sized sands have previously been used in their respective layers. As there is a tendency of the light gravel to rise and float, with the fine sand directly on the gravel of 1/8 to le", a mixing of A the same took place, and in the hope of avoiding this, deep beds were utilized.
The invention enables shallow gravel beds and relatively shallow sand beds to be used, by reason of thev provision of the intermediate layer of porous material of a constituency of relatively heavy specific gravity. The use of such an intermediate layer permits a higher velocity for the use of backwash water. l
Such an intermediate layer may beY of magnetite placed on the nest or top layer of gravel, and next below to the ne. eiective sand. The relative high specic gravity of the magnetite prevents the boiling of the gravel into it, and the intermixing of the fine sand with the magnetite. The Weight of such over intermediate layer thus acts to keep the strata formation of the layers of gravel and sand.
In other Words, in the old lters a gravel bed top layer of 1/8 to iig, the backwash-would lift the gravel and mix it with the Iine sand, whereas with a weighted intermediate layer, like magnetite, the lowergravel and upper sand layers remain in position as relatively fixed, and the fine sand can freely boil with the particles displaced from each other, whereby the impurities are readily removable.
The invention comprises a comparatively shallow graduated gravel bed supported by a perforated plate with a total area of openingsin the plate such as will cause Wash Water to pass through the openings at highvelocity, with a layer of heavier specific gravity constituents between the gravel layer and a superposed sand layer, whereby the intermediate layer acts as the nal point of water distribution into the iine sand uppermost layer, permitting the sand to boil andthe dirt to be washed out Without the intermediate layer moving or rising.
By the action described, an outlet cleaner, or dirty water take-off box, may discharge from each compartment the impurities thus separated, as a direct rflow `from below upwardly.
The invention will be further described, embodiments shown inthe drawing, and the essential features of the invention set forth in the appended claims.
In the accompanying drawing,
Fig. 1 is a perspective View partly in section of part of a lter apparatus, with a plurality of vertical compartments.
Fig. 2, a detail View of the backwash valve movable to close the lower end opening of each vertical compartment.
Fig. 3 is a vertical section through one vertical compartment showing the superposed layers of iilter material upon the perforated plate, in relation to the end opening,
Fig. 4 is a horizontal sectional detail of a pluralit;r of compartments, showing the dirty water take-oil box in one position in respect thereto.
Fig. is a similar View with the dirty water take-off box in another position, and
Fig. 6 is a similar View with the dirty water take-olf box in still another position.
Similar characters of reference indicate like parts.
Referring particularly to Fig. l, the lter apparatus there shown, is formed of a bottom wall IU, side walls I I and I2, end walls not being shown. Transversely of the apparatus, and perpendicular to the side walls I I and I2, are vertical partitions I3 which extend from side wall to side wall and divide the apparatus whatever may be its width between sidewall and sidewall, and whatever may be its length between endwall and endwall, into separate vertical compartments. About onethird of the height of the vertical partitions I3, suitable means I4 are provided for supporting perforated plates I5 which are horizontally disposed and form a perforated support extending from sidewall II to sidewall I2. Such means Ill may be secured to the vertical partitions and to the perforated plates. Angle irons I4A and MB support the plate I5, but any other suitable means may be provided, as the plate may be supported in any other suitable manner, as long as it is arranged about one-third or one-fourth up from the bottom wall I0.
In the embodiment shown, the vertical partitions are embedded in the bottom wall I0 but any other suitable iixing means may be utilized. The endwall II has a plurality of circular openings I6, spaced from each other, so that the center of said circular openings is eccentric with the geometrical center of the conguration formed by the perforated plate I5, the bottom I0 and the twointervening parts ISA and ISB of the partitions I3. The center is indicated by I1. Absolute accuracy of the disposition of the centers is not necessary, as the opening I6 can be arranged anywhere within the parts I5, I0 and I3A and I3B. A back wash valve guide I9 is arranged forming an eiliuent channel, which latter is adjacent the sidewall Il, and these guide walls I3 guide a valve which is movable longitudinally from end to end of the apparatus. has a pipe 2| supplied with a washing fluid, and has an opening 22 adapted to register with any of the openings I6 in the wall II. When communication between the openings I6 and 22 takes place, the washing water enters the opening I6 and flows into the lower part of the vertical compartment, and filling the lower part, the washing water rises in the compartment until it is about to overflow the same.
The vertical partitions I3, are provided at their upper ends with horizontally disposed plates 25 and upon them the dirty water take-oir' box 3! having two shoes 3| and 32 is slidable. The dirty water take-off box 3!) is moved from end to end of the apparatus, preferably periodically, to cover the open top of the vertical compartment which is being supplied at its bottom with washing water, and by means not shown in the drawing.
The irst improvement consists in providing each vertical compartment with an intermediate layer` of material of relatively high speciiic gravity between the layers of graded gravel and the layer of sand. In the embodiment of Fig. 3, three layers of gravel are shown, indicated by 40, 4I and 42. The lowermost layer 4U has gravel of 1/2" to The next superposed layer 4I is of gravel The valve 2B to 1/4", and the uppermost superposed layer 42 of gravel is of 1A," to 1/3". These gravel layers are held down by a layer of magnetite 43 or the like, of about 1/3 to j/16; and nally the top layer 4A is of sand. This sand layer extends only partially towards the uppermost ends I3c of the partitions, whereby a space is provided between the top surface of the sand and the horizontal partition 25. Magnetite has a higher specic gravity than gravel or sand, and thereby it acts as a stable intermediate layer stabilizing the gravel and sand layers.
The second improvement consists in the dirty water take-off box 30, in that it is connected with a suction producing apparatus (not shown) by a pipe 56, so that a suction action causes the impurities washed from the sand to be drawn into the dirty water take-off box 30. The box 30 has shoes 3| and 32 which rests upon the horizontal plates 25. This cooperation of the shoes and plates forms a seal, which prevents supernatant unfiltered liquors intermingling with and diluting the dirty wash water produced when the lter medium is backwashed. The vacuum action serves to draw the box down against the plate, and the liquid above the box serves to press the box down upon the plate. Between the shoes 3l and 32, two walls 33 and 34 incline upwardly and merge into a horizontal wall 35 having spaced openings 3S, which communicate with a conduit 31 which is in communication with the pipe 50. As suction is applied, the impurities resting upon the top sand layer or the boiling dirty water, are drawn into the space 38 of the box 30, and then into the conduit 31, and pipe 50 to some suitable place of discharge.
Figure 4 shows the relative position of the box 3E) in respect to one compartment, the suction box being on. This suction action and the consequent cleaning is contrary to the normal ltering action which has a descending action in that the fluid to be ltered is above the top sand layer and as the fluid descends through the top sand and layers below the same, the eiiluent finally reaches the space in the compartment below the perforated plate, and discharges through the opening I3 and into the eluent channel, leaving the impurities or other constituents in adsorption with the sand. This upward filter-cleaning action is clearly seen in Figures 4 and 5. It will be understood that while the cleansing action takes place, filtering is interrupted for the time being. The arrows 53 and 54 in Figures 4 and 5 show the normally downward filtering action taking place.
In Fig. 6, the opening I6 is provided with arrows 55 which show that the washing water enters the opening I6, and this fluid then rises through the gravel layers and layer of magnetite and top layer of sand, taking the adhering impurities with it until sucked in by the box 30 .as described. It is seen that there is a joint action between the vacuum action of the box 30 and the upward back wash action, brought about by the registering of the valve opening with the opening I6 of that particular vertical compartment.
In the filter beds heretofore used, the backwash action rising from the bottom of the bed caused the gravel of the gravel layers to intermingle with the sand, and this intermingling was accentuated by the suction action utilized to separate the impurities from the top layer of sand of the lter bed which also caused the sand to boil and to draw with it the gravel ofthe gravel layer immediately below the same. With the present invention, however, the intermediate layerv prevents interminglingof the gravel with the sand and, by virtue of its higher specic gravity yet porous characteristic, permits the passage of high-velocity fluidv therethrough without itself losing its layer-like or strata 'formation. In other words, this intermediate layer acts in the nature of a porous wall formed of material having a specific gravity higher than either the gravel below or vthe sand above, in whatever direction the iiow of fluid therethrough may be. y
Instead of magnetite, leaden bullets of suitable size can be used, orany vother material whose specific gravity is such that it is higher than the gravel particles to prevent them from rising to intermingle with the sand, and higher than the sand Aparticles to prevent the material of the intermediate layer from rising into the sand layer and mixing therewith. -Y
It will thus be seen that with the present invention, the efliciency and life of the filter beds are greatly increased by maintaining the sand and gravel layers in their respective stratas. The
weighted intermediate layer permits only the top sand layer to boil, withl the top surface of the sand normally'below the top edges of the vertical partitions. The sand particles thus entrained can vbe easily substituted by new sand particles'` supplied to take the place of those removed. The provision of the said space reduces the removal of the sand to a minimum.
A filter bed constructedin accordance with the present invention, in which a dirty water take-oi box removes the dirty water when the lter-bed is being subjected to backwashing from below upwardly, can be used in sewage treatment plants and will produce uniformly clean final effluents, the sand bed being a perfect floccing apparatus gathering the minute floc in a layer at the surface of the sand; such a bed can also be used in water treatment to remove algae and amorphous matter at high filter rates, and is especially adapted to filtration of water prior to the slow sand iilters because of the capacity and efliciency of the bed for removing solids, thus permitting an increased capacity and less frequent cleaning of the slow sand filters. The filter bed is especially adapted to swimming pools and similar purification installations because of the simple low pressure automatic operation and can easily be provided with means for chlorine dispersion. Furthermore the filter can be used for the recovery of products now going to waste, as
cleansing of liquors for re-use or to prevent poli lution, or can be used for any operation where a clean eiiluent is required.
From the foregoing it is believed that the construction and advantages of the present invention will be readily understood by those skilled in the art without further description, it being clear that changes may be made within the principle of the invention described without departing from the scope thereof as set out in the following claims.
What is claimed is:
1. In filter apparatus of the type including a plurality of vertical compartments containing a lter bed for each of said compartments, comprising gravel strata in the lower portion of said compartments, a layer of sand in the upper portion of said compartments, and an intermediate layer of a specific gravity higher than the gravel and sand interposed between said gravel strata and said layer of sand for preventing intermingling of said sand' and gravelduring the cleaning operation of said iilter bed, means 'for periodically? backwash cleaning said filterinaterial from theunderside of saidv compartments upwardly, means-supplying saidfbackwash cleaning means with backwash liquid, means straddling only the top of the compartment being cleaned forreceiving the backwash water, and leavingadjacent compartments uncovered,'and inlet and outlet filtering liquid means. 4
2;In filter apparatus of the typev including a pluralityof shallow vertical compartments, each containing iiltering material in the form of' a filter bed for each of said compartments comprising a gravel strata in the bottom ofv said compartments, and a sand strata in the upper portion of said compartments, and an intermediate weighted strata of material for maintainring said gravel andv said sandk in their respective stratas during the backwash cleaning operation of said filter apparatus, means for periodically backwash cleaning said filtering materialfrom the under-side of said compartments to the upper part thereof; backwash supply means, backwash removal means straddling one only of the compartments, the one being subjected to backwashing, inlet means for the iiuid to be ltered, and filtered liquid exit means, each of the compartments being like the other and capable of being connected with the backwash supply means,` and withfthe top straddling means, the top straddling means being capable of sliding from the top Vof onel compartment to the top of another compartment. v
3. In combination, a plurality of parallel upright walls, horizontal walls at right angles thereto, a box over the top edges of said two adjacent upright walls and the connecting longitudinal wall, means for forming a suction within the box and between two adjacent upright walls, a lter material between said walls, a backwash supply for said filter material, a backwash outlet for said box, a supply of the liquid to be filtered, and an outlet for the iiltrate, said suction causing the box to be pressed against the horizontal walls, whereby a sealing action between two adjacent longitudinal walls and the box is obtained, and the backwash is drawn from the lter material to the backwash outlet without mixing with the liquid being filtered.
4. In filtering apparatus including a iilter bed consisting of superposed layers of gravel and sand; an inlet for the unfiltered liquid supplied to and above the filter bed and an outlet for the filtered liquid coming from below the filter bed, said Iilter bed being between said inlet and outlet, the combination of backwash supply means below the filter bed, backwash outlet means above said lter bed, and between said backwash supply and outlet means therefor, and a layer of material disposed between said sand and gravel and having a specific gravity higher than that of said sand for preventing intermixture of the gravel with the sand both during the filtering and during the backwashing action.
5. In filtering apparatus of the type including a plurality of vertical compartments, each containing a filter bed comprising superposed layers of gravel and of sand, and an intermediate layer of material of higher specific gravity than said sand interposed between said first named layers for preventing intermingling of said sand and said gravel during the movement of the liquid in an upward direction through said lter bed, means for periodically backwash cleaning said ltering material from the underside of said compartments, suction removal means of the dirty wash-water at the upper end of the. compartment being backwashed, and inlets and outlets for the filtering liquids, the relative vspecific gravity of said material and said sand being such that upon the ow of the backwash upwardly through the lter bed, the sand material remains in layer form without substantial intermingling with the higher specific gravity material during its boiling necessary to remove its impurities, and said sand, said material, and said gravel remaining in layer form during the downward iiow ltering operation.
6. In a filter apparatus having a bottom, side and end walls including a plurality of open top channels parallel with each other from end Wall to end wall, a horizontal transverse perforated plate in each channel intermediate its top and bottom, a filter bed supported by each plate, said lter bed consisting of superposed layers of material graduated in respect to specic gravity, one of said interposed layers being of higher specific gravity than the layer above it, in combination therewith of a launder at right angles to the channels having an oriiice communicating with each channel into which filtered liquor from below the plate of the channel enters, backwash means travelling in the launder for forcing a required portion of fluid through an orifice and upwardly from the bottom and through the plate of a channel, means over the channel being back- Washed for removal from the top of the channel of the dirty Wash water as produced by the backwash means without intermingling of such dirty wash water with the supernatant and unltered liquid of adjacent channels, means connecting the backwash means with the removal means, means for moving the backwash means and removal means in unison from channel to channel, inlet means for the liquid to be ltered, outlet means for the filtrate, and backwash inlet and outlet means.
'7. In a filter apparatus having a bottom, side and end walls, a plurality of partitions extending vertically upwardly from said bottom and spaced from each other from end wall to end wall and extending from side wall to side wall, horizontally disposed perforated Walls intermediate the top and bottom ends of said partitions, and a filter material held on said perforated Walls, the combination therewith of horizontally aligned top plates upon each upper end of the said partitions, a dirty water take-off box having enclosing walls spaced substantially equal to the space between the aligned top plates for forming a closed space over two adjacent partitions, a pair of shoes on said box spaced the distance between said top plates and extending over said top plates -for sliding on said top plates, said pair of spaced shoes forming a seal with a pair of said spaced top plates when the box covers the open end of adjacent partitions, means supplying the iluid to be ltered above said partitions and said box, and means supplying a fluid below the filter material for passage to said take-olf box.
WILLIAM C. LAUGHLIN.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US343062A US2302450A (en) | 1940-06-29 | 1940-06-29 | Filter |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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US343062A US2302450A (en) | 1940-06-29 | 1940-06-29 | Filter |
Publications (1)
Publication Number | Publication Date |
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US2302450A true US2302450A (en) | 1942-11-17 |
Family
ID=23344522
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US343062A Expired - Lifetime US2302450A (en) | 1940-06-29 | 1940-06-29 | Filter |
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US (1) | US2302450A (en) |
Cited By (41)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3080062A (en) * | 1959-01-22 | 1963-03-05 | Raymond E Hebert | Filters |
US3236367A (en) * | 1961-08-21 | 1966-02-22 | Beckman Instruments Inc | Ion exchange resin column and method of stabilizing same |
US3239061A (en) * | 1963-06-05 | 1966-03-08 | Koppers Co Inc | Automatic backwash sand filter and process of cleaning same |
US3349918A (en) * | 1963-12-13 | 1967-10-31 | Kiyohiko Iki | Magnetizable-particle type filtration apparatus capable of performing continuous filtering operation |
US3437207A (en) * | 1963-10-10 | 1969-04-08 | Asea Ab | Means for purifying water |
US3459302A (en) * | 1967-04-25 | 1969-08-05 | Hydro Clear Corp | Apparatus and method of filtering solids from a liquid effluent |
US3512650A (en) * | 1969-07-15 | 1970-05-19 | Hirsch Abraham A | Method for installation of blended granular filter bed layers |
US3596768A (en) * | 1969-10-10 | 1971-08-03 | George R Whitten Jr | Apparatus for water purification |
USRE28458E (en) * | 1967-04-25 | 1975-07-01 | Apparatus and method of filtering solids from a liquid effluent | |
US3984326A (en) * | 1973-11-26 | 1976-10-05 | Pista S.A. | Gravity filtering equipment |
US4133766A (en) * | 1977-03-11 | 1979-01-09 | Koppers Company, Inc. | Filter media support and containment system |
US4152265A (en) * | 1977-08-19 | 1979-05-01 | Aqua-Aerobic Systems, Inc. | Filter apparatus |
FR2445734A1 (en) * | 1979-01-08 | 1980-08-01 | Environmental Elements Corp | Multicelled granular filter - fabricated of plastics to facilitate construction and reduce wt. |
US4450077A (en) * | 1982-08-06 | 1984-05-22 | Envirotech Corporation | Granular media filter |
US4454033A (en) * | 1981-09-29 | 1984-06-12 | Norbertus Verduyn | Filtering apparatus |
US4454034A (en) * | 1983-05-19 | 1984-06-12 | Aqua-Aerobic Systems, Inc. | Filter apparatus |
US4540487A (en) * | 1984-05-29 | 1985-09-10 | Aqua-Aerobic Systems, Inc. | Filter apparatus |
US4859330A (en) * | 1988-10-11 | 1989-08-22 | Davis Water & Waste Industries, Inc. | Traveling bridge filter with air scour |
US4957631A (en) * | 1989-01-26 | 1990-09-18 | Davis Water And Waste Industries, Inc. | Traveling bridge filter with surface wash |
US4988439A (en) * | 1989-02-27 | 1991-01-29 | Davis Water & Waste Industries, Inc. | Two stage traveling bridge filter |
US5089130A (en) * | 1990-11-26 | 1992-02-18 | Infilco Degremont Inc. | Filter cell sheet installations |
US5108614A (en) * | 1989-05-10 | 1992-04-28 | Serrener Consultation Inc. | Device and a method for filtering a liquid with wood ash to remove impurities therefrom |
US5256299A (en) * | 1990-07-02 | 1993-10-26 | International Environmental Systems, Inc., Usa | Method and apparatus for liquid treatment |
US5431809A (en) * | 1994-01-11 | 1995-07-11 | Davis Water & Waste Industries, Inc. | Apparatus for sealing a traveling bridge filter backwash shoe |
US5476584A (en) * | 1993-10-14 | 1995-12-19 | Davis Water & Waste Industries, Inc. | Backwash/rewash traveling bridge filter and related process |
US5512174A (en) * | 1993-05-28 | 1996-04-30 | Degremont | Filtering device for the clarification of liquids |
US5554281A (en) * | 1993-05-28 | 1996-09-10 | Davis Water & Waste Industries, Inc. | Traveling bridge filter system and associated underdrain |
US5599459A (en) * | 1994-01-11 | 1997-02-04 | Davis Water & Waste Industries, Inc. | Method for sealing a traveling bridge filter backwash shoe |
US5618421A (en) * | 1996-02-26 | 1997-04-08 | Infilco Degremont Inc. | Underdrain filter plate installations in automatic backwash filter systems |
WO1998001205A1 (en) * | 1996-07-08 | 1998-01-15 | United States Filter Corporation | Sealing shoe for celless traveling bridge filter |
US6245243B1 (en) | 1999-10-07 | 2001-06-12 | Meurer Industries, Inc. | Settler plate supports with integral outlets for individual flow channels and methods of collecting liquid from each flow channel |
US6616852B2 (en) * | 2001-06-28 | 2003-09-09 | Rg Delaware, Inc. | Modular filter system |
US20040055944A1 (en) * | 2002-06-18 | 2004-03-25 | Ondeo Degremont, Inc. | Filtration system underdrain |
US20040149641A1 (en) * | 2003-01-31 | 2004-08-05 | Roberts R. Lee | Modular filter system and method of repairing and/or replacing components thereof |
US20060006114A1 (en) * | 2004-07-08 | 2006-01-12 | Deskins Franklin D | Process for combining solids thickening and dewatering in one vessel |
US7314572B1 (en) | 2006-02-14 | 2008-01-01 | Meurer Research, Inc. | Methods of and apparatus for low-angle-tray settling with multi-zone configuration |
US20090166277A1 (en) * | 2000-11-06 | 2009-07-02 | Nihon Genryo Co., Ltd. | Method of cleansing filtration media and system thereof |
US7560035B1 (en) | 2007-06-22 | 2009-07-14 | Charles Lonnie Meurer | Overhead trough with constant trough flow velocity configuration and methods of regulating trough flow velocity |
US7718076B1 (en) | 2006-02-14 | 2010-05-18 | Charles Lonnie Meurer | Methods of and common gantry drive for single-pass cleaning of multiple stages of a material separation and removal system |
US7780015B1 (en) | 2006-08-24 | 2010-08-24 | Meurer Research, Inc. | Methods of and sludge collector with adjacent opposed oppositely-moving blades for moving sludge in a basin |
US20160114265A1 (en) * | 2012-02-12 | 2016-04-28 | Ide Technologies Ltd. | Integrated unit for intake and pretreatment with local backwashing |
-
1940
- 1940-06-29 US US343062A patent/US2302450A/en not_active Expired - Lifetime
Cited By (52)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3080062A (en) * | 1959-01-22 | 1963-03-05 | Raymond E Hebert | Filters |
US3236367A (en) * | 1961-08-21 | 1966-02-22 | Beckman Instruments Inc | Ion exchange resin column and method of stabilizing same |
US3239061A (en) * | 1963-06-05 | 1966-03-08 | Koppers Co Inc | Automatic backwash sand filter and process of cleaning same |
US3437207A (en) * | 1963-10-10 | 1969-04-08 | Asea Ab | Means for purifying water |
US3349918A (en) * | 1963-12-13 | 1967-10-31 | Kiyohiko Iki | Magnetizable-particle type filtration apparatus capable of performing continuous filtering operation |
US3459302A (en) * | 1967-04-25 | 1969-08-05 | Hydro Clear Corp | Apparatus and method of filtering solids from a liquid effluent |
USRE28458E (en) * | 1967-04-25 | 1975-07-01 | Apparatus and method of filtering solids from a liquid effluent | |
US3512650A (en) * | 1969-07-15 | 1970-05-19 | Hirsch Abraham A | Method for installation of blended granular filter bed layers |
US3596768A (en) * | 1969-10-10 | 1971-08-03 | George R Whitten Jr | Apparatus for water purification |
US3984326A (en) * | 1973-11-26 | 1976-10-05 | Pista S.A. | Gravity filtering equipment |
US4133766A (en) * | 1977-03-11 | 1979-01-09 | Koppers Company, Inc. | Filter media support and containment system |
US4152265A (en) * | 1977-08-19 | 1979-05-01 | Aqua-Aerobic Systems, Inc. | Filter apparatus |
FR2445734A1 (en) * | 1979-01-08 | 1980-08-01 | Environmental Elements Corp | Multicelled granular filter - fabricated of plastics to facilitate construction and reduce wt. |
US4454033A (en) * | 1981-09-29 | 1984-06-12 | Norbertus Verduyn | Filtering apparatus |
US4450077A (en) * | 1982-08-06 | 1984-05-22 | Envirotech Corporation | Granular media filter |
US4454034A (en) * | 1983-05-19 | 1984-06-12 | Aqua-Aerobic Systems, Inc. | Filter apparatus |
US4540487A (en) * | 1984-05-29 | 1985-09-10 | Aqua-Aerobic Systems, Inc. | Filter apparatus |
US4859330A (en) * | 1988-10-11 | 1989-08-22 | Davis Water & Waste Industries, Inc. | Traveling bridge filter with air scour |
US4957631A (en) * | 1989-01-26 | 1990-09-18 | Davis Water And Waste Industries, Inc. | Traveling bridge filter with surface wash |
US4988439A (en) * | 1989-02-27 | 1991-01-29 | Davis Water & Waste Industries, Inc. | Two stage traveling bridge filter |
US5108614A (en) * | 1989-05-10 | 1992-04-28 | Serrener Consultation Inc. | Device and a method for filtering a liquid with wood ash to remove impurities therefrom |
US5256299A (en) * | 1990-07-02 | 1993-10-26 | International Environmental Systems, Inc., Usa | Method and apparatus for liquid treatment |
US5089130A (en) * | 1990-11-26 | 1992-02-18 | Infilco Degremont Inc. | Filter cell sheet installations |
US5554281A (en) * | 1993-05-28 | 1996-09-10 | Davis Water & Waste Industries, Inc. | Traveling bridge filter system and associated underdrain |
US5512174A (en) * | 1993-05-28 | 1996-04-30 | Degremont | Filtering device for the clarification of liquids |
US5476584A (en) * | 1993-10-14 | 1995-12-19 | Davis Water & Waste Industries, Inc. | Backwash/rewash traveling bridge filter and related process |
US5545334A (en) * | 1994-01-11 | 1996-08-13 | Davis Water & Waste Industries, Inc. | Method for sealing a traveling bridge filter backwash shoe |
US5431809A (en) * | 1994-01-11 | 1995-07-11 | Davis Water & Waste Industries, Inc. | Apparatus for sealing a traveling bridge filter backwash shoe |
US5599459A (en) * | 1994-01-11 | 1997-02-04 | Davis Water & Waste Industries, Inc. | Method for sealing a traveling bridge filter backwash shoe |
US5618421A (en) * | 1996-02-26 | 1997-04-08 | Infilco Degremont Inc. | Underdrain filter plate installations in automatic backwash filter systems |
WO1998001205A1 (en) * | 1996-07-08 | 1998-01-15 | United States Filter Corporation | Sealing shoe for celless traveling bridge filter |
US5792359A (en) * | 1996-07-08 | 1998-08-11 | U.S. Filter Corporation | Sealing shoe for celless travelling bridge filter |
US6245243B1 (en) | 1999-10-07 | 2001-06-12 | Meurer Industries, Inc. | Settler plate supports with integral outlets for individual flow channels and methods of collecting liquid from each flow channel |
US20090166277A1 (en) * | 2000-11-06 | 2009-07-02 | Nihon Genryo Co., Ltd. | Method of cleansing filtration media and system thereof |
US6616852B2 (en) * | 2001-06-28 | 2003-09-09 | Rg Delaware, Inc. | Modular filter system |
US7090771B2 (en) * | 2002-06-18 | 2006-08-15 | Infilco Degremont, Inc. | Filtration system underdrain |
US20040055944A1 (en) * | 2002-06-18 | 2004-03-25 | Ondeo Degremont, Inc. | Filtration system underdrain |
US6942795B2 (en) | 2003-01-31 | 2005-09-13 | Rg Delaware, Inc. | Modular filter system and method of repairing and/or replacing components thereof |
US20040149641A1 (en) * | 2003-01-31 | 2004-08-05 | Roberts R. Lee | Modular filter system and method of repairing and/or replacing components thereof |
US7691261B2 (en) * | 2004-07-08 | 2010-04-06 | Franklin David Deskins | Apparatus for combining solids thickening and dewatering in one vessel |
US7494592B2 (en) * | 2004-07-08 | 2009-02-24 | Franklin David Deskins | Process for combining solids thickening and dewatering in one vessel |
US20090127180A1 (en) * | 2004-07-08 | 2009-05-21 | Franklin David Deskins | Process for combining solids thickening and dewatering in one vessel |
US20060006114A1 (en) * | 2004-07-08 | 2006-01-12 | Deskins Franklin D | Process for combining solids thickening and dewatering in one vessel |
US7314572B1 (en) | 2006-02-14 | 2008-01-01 | Meurer Research, Inc. | Methods of and apparatus for low-angle-tray settling with multi-zone configuration |
US7718076B1 (en) | 2006-02-14 | 2010-05-18 | Charles Lonnie Meurer | Methods of and common gantry drive for single-pass cleaning of multiple stages of a material separation and removal system |
US7780015B1 (en) | 2006-08-24 | 2010-08-24 | Meurer Research, Inc. | Methods of and sludge collector with adjacent opposed oppositely-moving blades for moving sludge in a basin |
US20110005998A1 (en) * | 2006-08-24 | 2011-01-13 | Meurer Research Inc. | Methods of and sludge collector with adjacent opposed oppositely-moving blades for moving sludge in a basin |
US7981302B2 (en) | 2006-08-24 | 2011-07-19 | Meurer Research Inc. | Method and apparatus for enhanced settling and collection of settled material |
US8074810B2 (en) | 2006-08-24 | 2011-12-13 | Meurer Research, Inc. | Methods of and sludge collector with adjacent opposed oppositely-moving blades for moving sludge in a basin |
US7560035B1 (en) | 2007-06-22 | 2009-07-14 | Charles Lonnie Meurer | Overhead trough with constant trough flow velocity configuration and methods of regulating trough flow velocity |
US20160114265A1 (en) * | 2012-02-12 | 2016-04-28 | Ide Technologies Ltd. | Integrated unit for intake and pretreatment with local backwashing |
US10926201B2 (en) * | 2012-02-12 | 2021-02-23 | Ide Technologies Ltd. | Integrated unit for intake and pretreatment with local backwashing |
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